Recovery of Nickel from Electroplating Wastewater Using Fluidized Bed Granulation Process(FBG)

碩士 === 嘉南藥理大學 === 環境工程與科學系 === 103 === Electroplating industries generate wastewater that contains significant amount of heavy metals. The most common method to treat heavy metals in wastewater is chemical coagulation. However, the said treatment method produces large volume of sludge that subsequen...

Full description

Bibliographic Details
Main Authors: Yi-Jing Chen, 陳怡靜
Other Authors: Ming-Chun Lu
Format: Others
Language:zh-TW
Published: 2014
Online Access:http://ndltd.ncl.edu.tw/handle/t4c38b
id ndltd-TW-103CNUP0515003
record_format oai_dc
spelling ndltd-TW-103CNUP05150032019-09-10T03:32:35Z http://ndltd.ncl.edu.tw/handle/t4c38b Recovery of Nickel from Electroplating Wastewater Using Fluidized Bed Granulation Process(FBG) 以流體化床造粒技術回收電鍍廢水中鎳離子 Yi-Jing Chen 陳怡靜 碩士 嘉南藥理大學 環境工程與科學系 103 Electroplating industries generate wastewater that contains significant amount of heavy metals. The most common method to treat heavy metals in wastewater is chemical coagulation. However, the said treatment method produces large volume of sludge that subsequent processes and additional cost are needed on the operation. A relatively new method such as crystallization using fluidized bed reactor (FBR) is at growing interest as it lessen sludge production and increases the recovery of metals as solid crystals. Synthetic nickel-containing wastewater had been used in this study as the representative for heavy metals in electroplating industry. The effects of operating parameters such as molar ratio, pH and flow rate were investigated to find the optimum condition. Experimental results showed that jar test cannot accurately determine the optimum pH suitable in FBR. High hydraulic load in FBR increases crystals collisions that deform some of the crystals produced and that it would accumulate as part of the sludge in the reflux section signifying poorer metal removal than low hydraulic loading. Using different concentration, higher concentration of nickel-containing wastewater have higher removal rate than the lower concentration but excessive dosage will increase processing costs and it is not economically feasible. It was also found out in the experiment that crystal growth must be controlled within a certain size range. Larger crystals tend to have lower removal rate than smaller crystals because smaller particles are in greater number that provides larger surface area than bigger crystals. Chelating agents in the wastewater prevents crystal formation that it should be treated first before introducing into the fluidized bed reactor. The crystals produced in the experiment underwent structural elemental analysis and the main product was determined to be nickel. Through SEM observation of the surface structure of a two hundred-nanometer colloidal particulate levels were grouped together to form dense crystalline beads. Ming-Chun Lu 盧明俊 2014 學位論文 ; thesis 133 zh-TW
collection NDLTD
language zh-TW
format Others
sources NDLTD
description 碩士 === 嘉南藥理大學 === 環境工程與科學系 === 103 === Electroplating industries generate wastewater that contains significant amount of heavy metals. The most common method to treat heavy metals in wastewater is chemical coagulation. However, the said treatment method produces large volume of sludge that subsequent processes and additional cost are needed on the operation. A relatively new method such as crystallization using fluidized bed reactor (FBR) is at growing interest as it lessen sludge production and increases the recovery of metals as solid crystals. Synthetic nickel-containing wastewater had been used in this study as the representative for heavy metals in electroplating industry. The effects of operating parameters such as molar ratio, pH and flow rate were investigated to find the optimum condition. Experimental results showed that jar test cannot accurately determine the optimum pH suitable in FBR. High hydraulic load in FBR increases crystals collisions that deform some of the crystals produced and that it would accumulate as part of the sludge in the reflux section signifying poorer metal removal than low hydraulic loading. Using different concentration, higher concentration of nickel-containing wastewater have higher removal rate than the lower concentration but excessive dosage will increase processing costs and it is not economically feasible. It was also found out in the experiment that crystal growth must be controlled within a certain size range. Larger crystals tend to have lower removal rate than smaller crystals because smaller particles are in greater number that provides larger surface area than bigger crystals. Chelating agents in the wastewater prevents crystal formation that it should be treated first before introducing into the fluidized bed reactor. The crystals produced in the experiment underwent structural elemental analysis and the main product was determined to be nickel. Through SEM observation of the surface structure of a two hundred-nanometer colloidal particulate levels were grouped together to form dense crystalline beads.
author2 Ming-Chun Lu
author_facet Ming-Chun Lu
Yi-Jing Chen
陳怡靜
author Yi-Jing Chen
陳怡靜
spellingShingle Yi-Jing Chen
陳怡靜
Recovery of Nickel from Electroplating Wastewater Using Fluidized Bed Granulation Process(FBG)
author_sort Yi-Jing Chen
title Recovery of Nickel from Electroplating Wastewater Using Fluidized Bed Granulation Process(FBG)
title_short Recovery of Nickel from Electroplating Wastewater Using Fluidized Bed Granulation Process(FBG)
title_full Recovery of Nickel from Electroplating Wastewater Using Fluidized Bed Granulation Process(FBG)
title_fullStr Recovery of Nickel from Electroplating Wastewater Using Fluidized Bed Granulation Process(FBG)
title_full_unstemmed Recovery of Nickel from Electroplating Wastewater Using Fluidized Bed Granulation Process(FBG)
title_sort recovery of nickel from electroplating wastewater using fluidized bed granulation process(fbg)
publishDate 2014
url http://ndltd.ncl.edu.tw/handle/t4c38b
work_keys_str_mv AT yijingchen recoveryofnickelfromelectroplatingwastewaterusingfluidizedbedgranulationprocessfbg
AT chényíjìng recoveryofnickelfromelectroplatingwastewaterusingfluidizedbedgranulationprocessfbg
AT yijingchen yǐliútǐhuàchuángzàolìjìshùhuíshōudiàndùfèishuǐzhōngnièlízi
AT chényíjìng yǐliútǐhuàchuángzàolìjìshùhuíshōudiàndùfèishuǐzhōngnièlízi
_version_ 1719249291774525440